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Kinetic data on the esterification of acetic acid with isobutanol have been obtained from both the uncatalyzed and heterogeneously catalyzed reactions using a stirred batch reactor in dioxane. The equilibrium constant, which is independent of temperature ranging from 318 to 368K, was found to be 4. The uncatalyzed reaction was proved to be second-order reversible. In the presence of the catalyst,...
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